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11. 发明申请

WO2013016703A3 GASIFICATION SYSTEM AND METHOD 审中-公开
标题翻译：气化系统和方法
公开(公告)号：WO2013016703A3
公开(公告)日：2013-04-18
申请号：PCT/US2012048715
申请日：2012-07-27
申请人： RENTECH INC , JIANG WEIBIN , MCCOMISH BRUCE , BORUM BRYAN C , CARRYER BENJAMIN , IBSEN MARK , ROBERTSON MARK , ELROD ERIC , WEEKS SIM , WRIGHT HAROLD A
发明人： JIANG WEIBIN , MCCOMISH BRUCE , BORUM BRYAN C , CARRYER BENJAMIN , IBSEN MARK , ROBERTSON MARK , ELROD ERIC , WEEKS SIM , WRIGHT HAROLD A
IPC分类号： C10J3/48 , C07C1/04 , C10G2/00 , C10J3/72 , F02C3/28
CPC分类号： C10J3/466 , B01J19/00 , C01B3/583 , C01B2203/044 , C01B2203/047 , C01B2203/062 , C10G2/332 , C10J3/485 , C10J3/56 , C10J2300/0909 , C10J2300/0916 , C10J2300/0923 , C10J2300/093 , C10J2300/0946 , C10J2300/12 , C10J2300/1618 , C10J2300/1637 , C10J2300/165 , C10J2300/1659 , C10J2300/1671 , C10J2300/1807 , C10J2300/1823 , C10K3/00 , F02G3/00 , Y02E50/32 , Y02P20/129 , Y02P20/145
摘要： A system configured for the production of at least one product selected from the group consisting of syngas, Fischer-Tropsch synthesis products, power, and chemicals, the system comprising a dual fluidized bed gasification apparatus and at least one apparatus selected from power production apparatus configured to produce power from the gasification product gas, partial oxidation reactors configured for oxidation of at least a portion of the product gas, tar removal apparatus configured to reduce the amount of tar in the product gas, Fischer-Tropsch synthesis apparatus configured to produce Fischer-Tropsch synthesis products from at least a portion of the product gas, chemical production apparatus configured for the production of at least one non-Fischer-Tropsch product from at least a portion of the product gas, and dual fluidized bed gasification units configured to alter the composition of the product gas. Methods of operating the system are also provided.
摘要翻译：一种配置用于生产从由合成气，费 - 托合成产物，动力和化学制剂组成的组中选择的至少一种产物的系统，所述系统包括双流化床气化装置和至少一种选自配置的动力生产装置从气化产物气体产生能量;部分氧化反应器，配置用于氧化产物气体的至少一部分;焦油去除装置，配置成减少产物气体中的焦油量;费 - 托合成装置，配置为产生费 - 来自至少一部分产物气的托合成产物，配置用于从至少一部分产物气生产至少一种非费 - 托产物的化学生产装置，以及配置成改变产物气的至少一部分非费 - 托产物的双流化床气化装置产品气体的组成。还提供了操作系统的方法。

12. 发明申请

WO2010118022A3 SYSTEM AND METHOD FOR CONDITIONING BIOMASS-DERIVED SYNTHESIS GAS 审中-公开
标题翻译：用于调节生物量衍生合成气体的系统和方法
公开(公告)号：WO2010118022A3
公开(公告)日：2011-01-20
申请号：PCT/US2010030090
申请日：2010-04-06
申请人： RENTECH INC , CARRYER BENJAMIN H , ELROD ERIC R , IBSEN MARK D , WRIGHT HAROLD A , JOHNSON BRIAN K
发明人： CARRYER BENJAMIN H , ELROD ERIC R , IBSEN MARK D , WRIGHT HAROLD A , JOHNSON BRIAN K
IPC分类号： C10J1/24 , C10J1/00 , C10L3/00
CPC分类号： C01B3/36 , B01J23/745 , C01B13/0259 , C01B2203/0261 , C01B2203/062 , C01B2203/0894 , C01B2203/1241 , C01B2203/1247 , C10G2/332 , C10G2300/1011 , C10J2300/0909 , C10J2300/0916 , C10J2300/0959 , C10J2300/1618 , C10J2300/1659 , C10J2300/1884 , Y02P20/145 , Y02P20/52 , Y02P30/20
摘要： A thermal conversion process comprising: pyrolizing or gasifying a carbonaceous feedstock to produce a first synthesis gas having a first H2:CO ratio of less than a minimum value or greater than a maximum value; providing enriched oxygen; and subjecting the first synthesis gas to partial oxidation in the presence of at least a portion of the enriched oxygen to produce a conditioned synthesis gas having a desired ratio of H2:CO in the range of from the minimum value to the maximum value. A method of producing FT product liquids by providing a conditioned synthesis gas according to the process and producing FT product liquids by subjecting the conditioned synthesis gas to FT reaction under FT operating conditions. A system for carrying out the methods is also provided.
摘要翻译：一种热转化方法，包括：将含碳原料热解或气化以产生具有小于最小值或大于最大值的第一H 2 :CO比率的第一合成气; 提供富氧; 在富氧的至少一部分的存在下对第一合成气进行部分氧化，以产生在所述最小值与最大值范围内具有希望的H 2：CO 2比例的条件合成气。通过根据该方法提供调节合成气并通过在FT操作条件下对经调节的合成气进行FT反应来生产FT产物液体来生产FT产物液体的方法。还提供了一种用于执行方法的系统。

13. 发明申请

WO2009148951A3 STABLE FERROUS-FERRIC NITRATE SOLUTIONS FOR FISCHER-TROPSCH CATALYST PREPARATION 审中-公开
标题翻译：用于FISCHER-TROPSCH催化剂制备的稳定的富勒烯 - 硝酸盐溶液
公开(公告)号：WO2009148951A3
公开(公告)日：2010-04-15
申请号：PCT/US2009045634
申请日：2009-05-29
申请人： RENTECH INC , NIKRAD PANDURANG V , TAYLOR JESSE W , BLEY RICHARD A , DUBUISSON DANNY M , ROLFE SARA L , DEMIREL BELMA , DUVENHAGE DAWID J , WRIGHT HAROLD A
发明人： NIKRAD PANDURANG V , TAYLOR JESSE W , BLEY RICHARD A , DUBUISSON DANNY M , ROLFE SARA L , DEMIREL BELMA , DUVENHAGE DAWID J , WRIGHT HAROLD A
IPC分类号： B01J27/25 , B01J23/745 , B01J37/03 , C01B21/50 , C01G49/00
CPC分类号： B01J35/002 , B01J23/002 , B01J23/745 , B01J23/78 , B01J37/03 , B01J37/10 , B01J2523/00 , C07C1/044 , C07C1/0445 , C10G2/332 , B01J2523/13 , B01J2523/17 , B01J2523/41 , B01J2523/842
摘要： A method of producing stable ferrous nitrate solution by dissolving iron in nitric acid to form a ferrous nitrate solution and maintaining the solution at a first temperature for a first time period, whereby the Fe(II) content of the ferrous nitrate solution changes by less than about 2% over a second time period. A method of producing stable Fe(II)/Fe(III) nitrate solution comprising ferrous nitrate and ferric nitrate and having a desired ratio of ferrous iron to ferric iron, including obtaining a stable ferrous nitrate solution; dissolving iron in nitric acid to form a ferric nitrate solution; maintaining the ferric nitrate solution at a second temperature for a third time period; and combining amounts of stable ferrous nitrate solution and ferric nitrate solution to produce the stable Fe(II)/Fe(III) nitrate solution. A method of preparing an iron catalyst is also described.
摘要翻译：通过将铁溶解在硝酸中以形成硝酸亚铁溶液并将溶液保持在第一温度第一时间的方式生产稳定的硝酸亚铁溶液的方法，由此硝酸亚铁溶液中的Fe（II）含量变化小于约2％在第二时期。制备包含硝酸亚铁和硝酸铁的稳定的Fe（II）/ Fe（III）硝酸盐溶液并具有所需比例的亚铁与三价铁的方法，包括获得稳定的硝酸亚铁溶液; 将铁溶解在硝酸中形成硝酸铁溶液; 将硝酸铁溶液在第二温度下保持第三次; 并加入稳定的硝酸亚铁溶液和硝酸铁溶液，制得稳定的Fe（II）/ Fe（III）硝酸盐溶液。还描述了制备铁催化剂的方法。

14. 发明申请

WO2013016702A3 GASIFICATION SYSTEM AND METHOD 审中-公开
公开(公告)号：WO2013016702A3
公开(公告)日：2013-05-02
申请号：PCT/US2012048714
申请日：2012-07-27
申请人： RENTECH INC , JIANG WEIBIN , MCCOMISH BRUCE , BORUM BRYAN C , CARRYER BENJAMIN , IBSEN MARK , ROBERTSON MARK , ELROD ERIC , WEEKS SIM , WRIGHT HAROLD A
发明人： JIANG WEIBIN , MCCOMISH BRUCE , BORUM BRYAN C , CARRYER BENJAMIN , IBSEN MARK , ROBERTSON MARK , ELROD ERIC , WEEKS SIM , WRIGHT HAROLD A
IPC分类号： C10J3/48 , C07C1/04 , C10G2/00 , C10J3/72 , C10J3/84
CPC分类号： C10J3/466 , B01J19/00 , C01B3/583 , C01B2203/044 , C01B2203/047 , C01B2203/062 , C10G2/332 , C10J3/485 , C10J3/56 , C10J2300/0909 , C10J2300/0916 , C10J2300/0923 , C10J2300/093 , C10J2300/0946 , C10J2300/12 , C10J2300/1618 , C10J2300/1637 , C10J2300/165 , C10J2300/1659 , C10J2300/1671 , C10J2300/1807 , C10J2300/1823 , C10K3/00 , F02G3/00 , Y02E50/32 , Y02P20/129 , Y02P20/145
摘要： A system configured for the production of at least one product selected from the group consisting of syngas, Fischer-Tropsch synthesis products, power, and chemicals, the system comprising a dual fluidized bed gasification apparatus and at least one apparatus selected from power production apparatus configured to produce power from the gasification product gas, partial oxidation reactors configured for oxidation of at least a portion of the product gas, tar removal apparatus configured to reduce the amount of tar in the product gas, Fischer-Tropsch synthesis apparatus configured to produce Fischer-Tropsch synthesis products from at least a portion of the product gas, chemical production apparatus configured for the production of at least one non-Fischer-Tropsch product from at least a portion of the product gas, and dual fluidized bed gasification units configured to alter the composition of the product gas. Methods of operating the system are also provided.

15. 发明申请

WO2009032701A3 STRENGTHENED IRON CATALYST FOR SLURRY REACTORS 审中-公开
标题翻译：用于浆料反应器的强化铁催化剂
公开(公告)号：WO2009032701A3
公开(公告)日：2009-05-07
申请号：PCT/US2008074484
申请日：2008-08-27
申请人： RENTECH INC , BENHAM CHARLES B , FRAENKEL DAN , BLEY RICHARD A , TAYLOR JESSE W , DEMIREL BELMA , ROLFE SARA L , WRIGHT HAROLD A
发明人： DEMIREL BELMA , ROLFE SARA L , WRIGHT HAROLD A
IPC分类号： B01J23/78 , C07C27/06
CPC分类号： B01J23/78 , B01J21/005 , B01J21/08 , B01J37/03 , C10G2/331 , C10G2300/70
摘要： A method of strengthening a precipitated unsupported iron catalyst by: preparing a precipitated unsupported iron catalyst containing copper and potassium; adding a solution comprising a structural promoter to the previously prepared catalyst; drying the mixture; and calcining the dried catalyst. A method for preparing an iron catalyst, the method comprising: precipitating a catalyst precursor comprising iron phases selected from hydroxides, oxides, and carbonates; adding a promoter to the catalyst precursor to yield a promoted precursor; drying the promoted precursor to yield dried catalyst; and calcining the dried catalyst, wherein the catalyst further comprises copper and potassium. A method of preparing a strengthened precipitated iron catalyst comprising: co-precipitating iron, copper, magnesium, and aluminum; washing the precipitate; alkalizing the precipitate; and drying the precipitate to yield a dried catalyst precursor. The dried catalyst precursor may be calcined and treated with a gas comprising carbon monoxide.
摘要翻译：一种通过以下方法强化沉淀的无载体铁催化剂：制备沉淀的含铜和钾的无载体铁催化剂; 向先前制备的催化剂中加入包含结构促进剂的溶液; 干燥混合物; 并煅烧干燥的催化剂。一种制备铁催化剂的方法，所述方法包括：沉淀包含选自氢氧化物，氧化物和碳酸盐的铁相的催化剂前体; 向催化剂前体中加入促进剂以产生促进的前体; 干燥促进的前体以产生干燥的催化剂; 并煅烧所述干燥的催化剂，其中所述催化剂还包含铜和钾。一种制备强化沉淀铁催化剂的方法，包括：共沉淀铁，铜，镁和铝; 洗涤沉淀物; 使沉淀物碱化; 并干燥沉淀物，得到干燥的催化剂前体。干燥的催化剂前体可以被煅烧并用包含一氧化碳的气体处理。

16. 发明申请

WO2013016704A3 GASIFICATION SYSTEM AND METHOD 审中-公开
公开(公告)号：WO2013016704A3
公开(公告)日：2013-04-18
申请号：PCT/US2012048717
申请日：2012-07-27
申请人： RENTECH INC , JIANG WEIBIN , MCCOMISH BRUCE , BORUM BRYAN C , CARRYER BENJAMIN , IBSEN MARK , ROBERTSON MARK , ELROD ERIC , WEEKS SIM , WRIGHT HAROLD A
发明人： JIANG WEIBIN , MCCOMISH BRUCE , BORUM BRYAN C , CARRYER BENJAMIN , IBSEN MARK , ROBERTSON MARK , ELROD ERIC , WEEKS SIM , WRIGHT HAROLD A
IPC分类号： C10J3/48 , C07C1/04 , C10G2/00 , C10J3/72 , F02C3/28
CPC分类号： C10J3/466 , B01J19/00 , C01B3/583 , C01B2203/044 , C01B2203/047 , C01B2203/062 , C10G2/332 , C10J3/485 , C10J3/56 , C10J2300/0909 , C10J2300/0916 , C10J2300/0923 , C10J2300/093 , C10J2300/0946 , C10J2300/12 , C10J2300/1618 , C10J2300/1637 , C10J2300/165 , C10J2300/1659 , C10J2300/1671 , C10J2300/1807 , C10J2300/1823 , C10K3/00 , F02G3/00 , Y02E50/32 , Y02P20/129 , Y02P20/145
摘要： A system configured for the production of at least one product selected from the group consisting of syngas, Fischer-Tropsch synthesis products, power, and chemicals, the system comprising a dual fluidized bed gasification apparatus and at least one apparatus selected from power production apparatus configured to produce power from the gasification product gas, partial oxidation reactors configured for oxidation of at least a portion of the product gas, tar removal apparatus configured to reduce the amount of tar in the product gas, Fischer-Tropsch synthesis apparatus configured to produce Fischer-Tropsch synthesis products from at least a portion of the product gas, chemical production apparatus configured for the production of at least one non-Fischer-Tropsch product from at least a portion of the product gas, and dual fluidized bed gasification units configured to alter the composition of the product gas. Methods of operating the system are also provided.

17. 发明申请

WO2013016706A2 GASIFICATION SYSTEM AND METHOD 审中-公开
标题翻译：气化系统及方法
公开(公告)号：WO2013016706A2
公开(公告)日：2013-01-31
申请号：PCT/US2012048719
申请日：2012-07-27
申请人： RENTECH INC , JIANG WEIBIN , MCCOMISH BRUCE , BORUM BRYAN C , CARRYER BENJAMIN , IBSEN MARK , ROBERTSON MARK , ELROD ERIC , WEEKS SIM , WRIGHT HAROLD A
发明人： JIANG WEIBIN , MCCOMISH BRUCE , BORUM BRYAN C , CARRYER BENJAMIN , IBSEN MARK , ROBERTSON MARK , ELROD ERIC , WEEKS SIM , WRIGHT HAROLD A
IPC分类号： C10J3/46 , B01J19/00 , C07C1/04 , C10G2/00
CPC分类号： C10J3/466 , B01J19/00 , C01B3/583 , C01B2203/044 , C01B2203/047 , C01B2203/062 , C10G2/332 , C10J3/485 , C10J3/56 , C10J2300/0909 , C10J2300/0916 , C10J2300/0923 , C10J2300/093 , C10J2300/0946 , C10J2300/12 , C10J2300/1618 , C10J2300/1637 , C10J2300/165 , C10J2300/1659 , C10J2300/1671 , C10J2300/1807 , C10J2300/1823 , C10K3/00 , F02G3/00 , Y02E50/32 , Y02P20/129 , Y02P20/145
摘要： A system configured for the production of at least one product selected from the group consisting of syngas, Fischer-Tropsch synthesis products, power, and chemicals, the system comprising a dual fluidized bed gasification apparatus and at least one apparatus selected from power production apparatus configured to produce power from the gasification product gas, partial oxidation reactors configured for oxidation of at least a portion of the product gas, tar removal apparatus configured to reduce the amount of tar in the product gas, Fischer-Tropsch synthesis apparatus configured to produce Fischer-Tropsch synthesis products from at least a portion of the product gas, chemical production apparatus configured for the production of at least one non-Fischer-Tropsch product from at least a portion of the product gas, and dual fluidized bed gasification units configured to alter the composition of the product gas. Methods of operating the system are also provided.
摘要翻译：一种被配置用于生产选自由合成气，费 - 托合成产物，动力和化学品组成的组中的至少一种产物的系统，所述系统包括双流化床气化装置和至少一种选自动力生产装置以产生来自气化产物气体的功率，构造成用于氧化产物气体的至少一部分的部分氧化反应器，被配置为减少产物气体中的焦油量的焦油去除装置，配置成产生费 - 托合成装置的费 - 托合成装置，来自产品气体的至少一部分的托合成产物，被配置用于从至少一部分产物气体生产至少一种非费 - 托产物的化学生产设备，以及被配置为改变产物气体的至少一部分的双流化床气化单元产品气体的组成。还提供了操作系统的方法。

18. 发明申请

WO2010059660A2 METHOD FOR ACTIVATING STRENGTHENED IRON CATALYST FOR SLURRY REACTORS 审中-公开
标题翻译：活化用于浆体反应器的铁催化剂的方法
公开(公告)号：WO2010059660A2
公开(公告)日：2010-05-27
申请号：PCT/US2009064895
申请日：2009-11-18
申请人： RENTECH INC , DEMIREL BELMA , BENHAM CHARLES B , FRAENKEL DAN , BLEY RICHARD , TAYLOR JESSE W , REJAI BAHMAN , ROLFE SARA L , WRIGHT HAROLD A
发明人： DEMIREL BELMA , BENHAM CHARLES B , FRAENKEL DAN , BLEY RICHARD , TAYLOR JESSE W , REJAI BAHMAN , ROLFE SARA L , WRIGHT HAROLD A
IPC分类号： B01J23/72 , B01J15/00 , B01J37/08
CPC分类号： B01J37/18 , B01J21/08 , B01J23/745 , B01J23/78 , B01J37/03 , C10G2/332 , C10G2300/4006 , C10G2300/703
摘要： A method of activating an iron Fischer-Tropsch catalyst by introducing an inert gas into a reactor comprising a slurry of the catalyst at a first temperature, increasing the reactor temperature from the first temperature to a second temperature at a first ramp rate, wherein the second temperature is in the range of from about 150°C to 250°C, introducing synthesis gas having a ratio of H2:CO to the reactor at a space velocity, and increasing the reactor temperature from the second temperature to a third temperature at a second ramp rate, wherein the third temperature is in the range of from about 270°C to 300°C. The iron Fischer-Tropsch catalyst may be a precipitated unsupported iron catalyst, production of which is also provided.
摘要翻译：通过在第一温度下将惰性气体引入反应器中来活化铁费 - 托催化剂的方法，所述反应器包含所述催化剂的浆料，以第一升温速率将反应器温度从第一温度升高至第二温度，温度在约150℃至250℃的范围内，以空间速度向反应器中引入具有H 2 :CO比率的合成气，并且将反应器温度从第二温度增加至第三温度斜率，其中第三温度在约270℃至300℃的范围内。铁费托催化剂可以是沉淀的未负载的铁催化剂，也提供其生产。

19. 发明申请

WO2009148952A2 STRENGTHENING IRON FISCHER-TROPSCH CATALYST BY CO-FEEDING IRON NITRATE AND PRECIPITATING AGENT OR SEPARATELY PRECIPITATING FROM FERROUS NITRATE AND FERRIC NITRATE SOLUTIONS 审中-公开
标题翻译：通过加入硝酸铁和预处理剂或分离地从硝酸盐和富含硝酸盐的溶液中分离加强铁离子捕获催化剂
公开(公告)号：WO2009148952A2
公开(公告)日：2009-12-10
申请号：PCT/US2009045636
申请日：2009-05-29
申请人： RENTECH INC , DEMIREL BELMA , TAYLOR JESSE W , NIKRAD PANDURANG V , ROLFE SARA L , DUVENHAGE DAWID J , WRIGHT HAROLD A
发明人： DEMIREL BELMA , TAYLOR JESSE W , NIKRAD PANDURANG V , ROLFE SARA L , DUVENHAGE DAWID J , WRIGHT HAROLD A
IPC分类号： B01J23/745 , B01J27/25 , B01J37/03
CPC分类号： B01J37/03 , B01J23/002 , B01J23/745 , B01J23/78 , B01J35/002 , B01J35/0033 , B01J35/1014 , B01J35/1019 , B01J35/1038 , B01J35/1042 , B01J35/1061 , B01J37/0045 , B01J2523/00 , C10G2/332 , B01J2523/13 , B01J2523/17 , B01J2523/41 , B01J2523/847
摘要： A method of producing a catalyst precursor comprising iron phases by co-feeding a ferrous nitrate solution and a precipitation agent into a ferric nitrate solution to produce a precipitation solution having a desired ferrous:ferric nitrate ratio and from which catalyst precursor precipitates; co-feeding a ferric nitrate solution and a precipitation agent into a ferrous nitrate solution to produce a precipitation solution having a desired ferrous:ferric nitrate ratio and from which catalyst precursor precipitates; or precipitating a ferrous precipitate from a ferrous nitrate solution by contacting the ferrous nitrate solution with a first precipitation agent; precipitating a ferric precipitate from ferric nitrate solution by contacting the ferric nitrate solution with a second precipitation agent and combining the ferrous and ferric precipitates to form the catalyst precursor, wherein the ratio of ferrous:ferric precipitates is a desired ratio.
摘要翻译：通过将硝酸亚铁溶液和沉淀剂通过将硝酸铁溶液共同加入到硝酸铁溶液中以产生具有所需的亚铁：硝酸铁比例并且催化剂前体沉淀的沉淀溶液来生产包含铁相的催化剂前体的方法; 将硝酸铁溶液和沉淀剂共同加入到硝酸亚铁溶液中以产生具有所需的亚铁：硝酸铁比例并且催化剂前体沉淀的沉淀溶液; 或通过使硝酸亚铁溶液与第一沉淀剂接触从硝酸亚铁溶液中沉淀出铁沉淀物; 通过使硝酸铁溶液与第二沉淀剂接触并将亚铁和铁沉淀物结合以形成催化剂前体，从而从硝酸铁溶液中沉淀出铁沉淀物，其中亚铁：铁析出物的比例为所需比例。

20. 发明申请

WO2013016705A3 GASIFICATION SYSTEM AND METHOD 审中-公开
公开(公告)号：WO2013016705A3
公开(公告)日：2013-04-18
申请号：PCT/US2012048718
申请日：2012-07-27
申请人： RENTECH INC , JIANG WEIBIN , MCCOMISH BRUCE , BORUM BRYAN C , CARRYER BENJAMIN , IBSEN MARK , ROBERTSON MARK , ELROD ERIC , WEEKS SIM , WRIGHT HAROLD A
发明人： JIANG WEIBIN , MCCOMISH BRUCE , BORUM BRYAN C , CARRYER BENJAMIN , IBSEN MARK , ROBERTSON MARK , ELROD ERIC , WEEKS SIM , WRIGHT HAROLD A
IPC分类号： C10J3/48 , C07C1/04 , C10G2/00 , C10J3/72 , F02C3/28
CPC分类号： C10J3/466 , B01J19/00 , C01B3/583 , C01B2203/044 , C01B2203/047 , C01B2203/062 , C10G2/332 , C10J3/485 , C10J3/56 , C10J2300/0909 , C10J2300/0916 , C10J2300/0923 , C10J2300/093 , C10J2300/0946 , C10J2300/12 , C10J2300/1618 , C10J2300/1637 , C10J2300/165 , C10J2300/1659 , C10J2300/1671 , C10J2300/1807 , C10J2300/1823 , C10K3/00 , F02G3/00 , Y02E50/32 , Y02P20/129 , Y02P20/145
摘要： A system configured for the production of at least one product selected from the group consisting of syngas, Fischer-Tropsch synthesis products, power, and chemicals, the system comprising a dual fluidized bed gasification apparatus and at least one apparatus selected from power production apparatus configured to produce power from the gasification product gas, partial oxidation reactors configured for oxidation of at least a portion of the product gas, tar removal apparatus configured to reduce the amount of tar in the product gas, Fischer-Tropsch synthesis apparatus configured to produce Fischer-Tropsch synthesis products from at least a portion of the product gas, chemical production apparatus configured for the production of at least one non-Fischer-Tropsch product from at least a portion of the product gas, and dual fluidized bed gasification units configured to alter the composition of the product gas. Methods of operating the system are also provided.

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